Inkjet inks containing crosslinked polyurethanes

ABSTRACT

Inkjet inks that have, as a principal component, a crosslinked polyurethane dispersoid binder additive with selected diols used to prepare the polyurethane. The diols include a polyether diol, an ionic diol and polycarbonate, polyamide and/or poly(meth)acrylate diols. These inks can be used for printing on different media, and are particularly suitable for printing on textiles. The printed textiles are particularly durable to wash fastness and crock.

CROSS-REFERENCE TO RELATED APPLICATION

This application claims priority under 35 U.S.C. §119 from U.S.Provisional Application Ser. No. 61/126,872, filed Mar. 8, 2008.

BACKGROUND OF THE INVENTION

This invention pertains to aqueous inkjet inks, more specifically topigmented inkjet inks containing one or more crosslinked polyurethanedispersoid binders produced from specific diols. These binders areparticularly suitable for use in textile printing inks. These inks areadvantageous because printed textiles made with these inks have improvedwashfastness and colorfastness. These binders also have improvedhydrolytic stability and consequently inks utilizing these binders haveimproved storage stability.

Suitable digital printing systems for textiles are disclosed in the art,for example, in commonly owned US20030128246 and US20030160851. Even asinkjet hardware improvements are made to increase printing speeds,adoption of inkjet printing in the textile industry will be impeded ifmethods to also improve colorfastness are not found.

A disadvantage of inkjet printing, in particular inkjet printing withpigmented ink, is inkjet printed fabrics are particularly susceptible tocolor removal by abrasion and thus have poor durability. Furthermore,another disadvantage of inkjet printing, in particular inkjet printingwith pigmented ink, is that inkjet printed fabrics do not toleratewashing conditions required for textiles. The printed colors both fadeupon washing and during the wash the colors can be undesirablytransferred to other fabrics in the wash or to the washing machineparts. Furthermore, inks made for commercial consumption must withstandextended periods of storage conditions. The inks cannot degrade eitherin ink properties or the properties of the resultant print.

Therefore, there is need for improved ink stability, as well as improveddurability of inkjet images on textile, especially in cases where thecolorant is pigment. It is thus an object of this invention to provideinkjet inks with improved storage stability and inkjet printed textileswith improved durability and colorfastness especially as a result oflaundering.

SUMMARY OF THE INVENTION

In an embodiment of the invention, stability of ink and the washfastnessof an inkjet printed textile can be improved to a commerciallyacceptable level by using a first crosslinked polyurethane dispersoidbinder in aqueous inkjet inks where the first crosslinked polyurethanehas an isocyanate reactive portion comprising a mixture of diols Z₁, Z₂and Z₃ (see below) or a physical mixture of at least a second and athird crosslinked polyurethane dispersoids where an isocyanate reactiveportion of the second polyurethane comprises a mixture of the diols Z₁,and Z₂ and an isocyanate reactive portion of the third polyurethanecomprises a mixture of the diols Z₂ and Z₃.

Each of the aforementioned crosslinked polyurethane dispersoidspreferably satisfy the condition that the amount of crosslinking in thecrosslinked polyurethanes is greater than about 1% and less than about50 wt % as measured by the THF insolubles test.

In one aspect of the present invention, there is provided an inkjet inkcomposition comprising an aqueous vehicle having a colorant and a firstcrosslinked polyurethane dispersoid, wherein the ink comprises the firstcrosslinked polyurethane dispersoid preferably in an amount greater thanabout 0.5% to about 30% by weight, based on the total weight of the ink,and wherein the amount of crosslinking in the first crosslinkedpolyurethane is greater than about 1% and less than about 50 wt % asmeasured by the THF insolubles test and where the first crosslinkedpolyurethane is formed from a first diol, Z₁ a second diol, Z₂ and athird diol Z₃ and

where

p greater than or equal to 2,and m greater than or equal to 3 to about 36;R₅, R₆=hydrogen, alkyl, substituted alkyl, aryl; where the R₅ or R₆ arethe same or different for each substituted methylene group and where R₅and R₅ or R₆ can be joined to form a cyclic structure;Z₂ is a diol substituted with an ionic group;Z₃ is selected from the group consisting of polycarbonate diols,polyamide diols and poly(meth)acrylate diols;and where the colorant is selected from pigments and dyes orcombinations of pigments and dyes.

In another embodiment, there is provided an inkjet ink compositioncomprising an aqueous vehicle having a colorant and a second crosslinkedpolyurethane dispersoid and a third crosslinked polyurethane dispersoid,wherein the ink comprises the second crosslinked polyurethane dispersoidpreferably in an amount greater than about 0.25% to about 30% by weightand the third crosslinked polyurethane dispersoid preferably in anamount greater than about 0.5% to about 30% by weight based on the totalweight of the ink, and wherein the amount of crosslinking in the secondcrosslinked polyurethane is greater than about 1% and less than about 50wt % based on the THF insolubles test and the amount of crosslinking inthe third crosslinked polyurethane is greater than about 1% and lessthan about 50 wt % based on the THF insolubles test and where the secondcrosslinked polyurethane is formed from a first diol, Z₁ and a seconddiol, Z₂ and the third crosslinked polyurethane is formed from a seconddiol, Z₂ and a third diol, Z₃ and where Z₁, Z₂ and Z₃ are as definedabove, and the colorant is selected from pigments and dyes orcombinations of pigments and dyes.

The instant invention is particularly advantageous for improving thedurability of textiles printed with colorants in inkjet inks, and allowsthe achievement of commercially acceptable durability for inkjet inkprinted textiles. In studies of the previously described, polyurethanebinders (US2005/0182154) were shown to have poor storage stability, andwhen used after storage, produced poorer washfastness and crock. It issurprising that both the chemical combination of all 3 diols, Z₁, Z₂ andZ₃, in the polyurethane and the physical mixtures of the diols taken twoat a time, Z₁ and Z₂ and Z₂ and Z₃ lead to the improved binderperformance.

The present invention also provides aqueous dispersions, preferablycolorant dispersions, which further contain dispersed crosslinkedpolyurethane dispersoid particles (as described above).

The invention also relates to a method of preparing the crosslinkedpolyurethane dispersoid (as set forth above). The first step in thepreparation is preparing an aqueous dispersion of an aqueous crosslinkedpolyurethane dispersoid composition comprising the steps:

(a) providing reactants comprising (i) at least one diol Z₃ or Z₁ asdefined above ii) at least one polyisocyanate component comprising adiisocyanate, and (iii) at least one hydrophilic reactant comprising atleast one isocyanate reactive ingredient containing an ionic group, Z₂as defined above;

(b) contacting (i), (ii) and (iii) in the presence of a water-miscibleorganic solvent to form an isocyanate-functional polyurethaneprepolymer;

(c) adding water to form an aqueous dispersion; and

(d) prior to, concurrently with or subsequent to step (c), providing acrosslinking component, chain extending, or chain-terminating theisocyanate-functional prepolymer with a primary or secondary amine.

The diol, diisocyanate and hydrophilic reactant may be added together inany order.

If the hydrophilic reactant contains ionizable groups then, at the timeof addition of water (step (c)), the ionizable groups must be ionized byadding acid or base (depending on the type of ionizable group) in anamount such that the polyurethane can be stably dispersed.

Preferably, at some point during the reaction (generally after additionof water and after crosslinking, chain extension or chain termination.),the organic solvent is substantially removed under vacuum to produce anessentially solvent-free dispersion.

In a further aspect embodiment, there is provided an inkjet inkcomposition comprising an aqueous vehicle, a colorant and one or morecrosslinked polyurethane dispersoid(s) that is/are formulated accordingto any of the specific diol combinations described above, wherein thecolorant is soluble or dispersible in the aqueous vehicle, and whereinthe weight ratio of the crosslinked polyurethane dispersoid(s) tocolorant is at least about 0.2. The inkjet ink may optionally compriseother well-known additives ts as required to obtain final desiredproperties of the ink or, in turn properties for the printed image.

The colorant in the inkjet ink preferably ranges from about 0.1 to about30 wt %, based on the total weight of the ink, and is preferably apigment. The crosslinked polyurethane dispersoid is preferably more thanabout 1% by weight, based on the total weight of the ink. When two ormore crosslinked polyurethane dispersoids are used the amount ofdispersoids is preferably more than about 1% by weight, based on thetotal weight of the ink. The amount of crosslinking in the crosslinkedpolyurethane(s) is preferably more than about 1 wt %, and less thanabout 50 wt % as measured by the THF insolubles test discussed infurther detail below.

In accordance with another aspect embodiment, there is provided aninkjet ink set comprising at least three differently colored inkjetinks, wherein at least one of the inks is an inkjet ink as set forthabove.

In yet another embodiment, there is provided a method for inkjetprinting onto a substrate, comprising the steps of:

(a) providing an inkjet printer that is responsive to digital datasignals;

(b) loading the printer with a substrate to be printed;

(c) loading the printer with an ink as set forth above and described infurther detail below, or an inkjet ink set as set forth above anddescribed in further detail below; and

(d) printing onto the substrate using the ink or inkjet ink set inresponse to the digital data signals.

As indicated above, the inks and ink sets in accordance with the presentinvention are particularly useful as inkjet inks, more particularly asinkjet inks for textile printing. Preferred substrates, therefore,include textiles. The printed textile can optionally be subject to afusing process after printing. The fusing process requires exposing theprinted textile to a combination of heat and pressure, which has beenfound to generally improve the durability of the textile, particularlywhen the colorant is a pigment. In particular, the post treatmentcombination of heat and pressure has been found to improve washfastnessand stain rating.

Another aspect of the present invention is an inkjet printed textileinkjet printed with a pigmented inkjet ink, said printed textile havinga wash fastness of at least 3 (as measured in accordance with AATCC TestMethod 61-1996 as the 3A test) and a crock rating of at least 3.5 (asmeasured by AATCC Test Method Alternatively, the washfastness can bemeasured by comparing the color of the print after printing and thenafter 3 wash cycles.

These and other features and advantages of the present invention will bemore readily understood by those of ordinary skill in the art from thefollowing Detailed Description. It is to be appreciated that certainfeatures of the invention which are, for clarity, described above andbelow in the context of separate embodiments, may also be provided incombination in a single embodiment. Conversely, various features of theinvention that are, for brevity, described in the context of a singleembodiment, may also be provided separately or in any subcombination.

DETAILED DESCRIPTION

Unless otherwise defined, all technical and scientific terms used hereinhave the same meaning as commonly understood by one of ordinary skill inthe art to which this invention belongs. In case of conflict, thepresent specification, including definitions, will control.

Unless stated otherwise, all percentages, parts, ratios, etc., are byweight.

When an amount, concentration, or other value or parameter is given aseither a range, preferred range or a list of upper preferable values andlower preferable values, this is to be understood as specificallydisclosing all ranges formed from any pair of any upper range limit orpreferred value and any lower range limit or preferred value, regardlessof whether ranges are separately disclosed. Where a range of numericalvalues is recited herein, unless otherwise stated, the range is intendedto include the endpoints thereof, and all integers and fractions withinthe range. It is not intended that the scope of the invention be limitedto the specific values recited when defining a range.

When the term “about” is used in describing a value or an end-point of arange, the disclosure should be understood to include the specific valueor end-point referred to.

The materials, methods, and examples herein are illustrative only and,except as specifically stated, are not intended to be limiting. Althoughmethods and materials similar or equivalent to those described hereincan be used in the practice or testing of the present invention,suitable methods and materials are described herein.

The aqueous inks comprise a colorant, a crosslinked polyurethanedispersoid binder and other ink components, wherein the colorant issoluble or dispersible in the aqueous vehicle.

In accordance with the present invention, the term “polyurethanedispersoid” refers to an aqueous dispersion/emulsion of a polymercontaining urethane groups (e.g., polyurethane), as those terms areunderstood by persons of ordinary skill in the art. The aqueouscrosslinked polyurethane dispersoid in accordance with the presentinvention comprises a crosslinked polyurethane, and thus is an aqueousstable polyurethane emulsion or dispersion in which the polyurethanecontains some crosslinking. To distinguish the polyurethanedispersions/emulsion binders from the other dispersions and componentsin the inkjet ink, they are referred to herein as polyurethane“dispersoid(s)”.

The crosslinked polyurethane dispersoid(s) is combined with the aqueousvehicle, colorant and other common ink jet components to produce astable inkjet ink that can be used to print on all substrates. Theseinks are especially useful for textiles. The crosslinked polyurethane(s)preferably has had all of its crosslinking completed prior to itsaddition to the other inkjet ink components. The order of addition ofthe ink components can be in any convenient order.

While not being bound by theory it is believed that the combination ofthe polyetherdiol (Z₁) and the selected diols described by Z₃ provides abinder system for the inks that produce a significantly improvedprinting performance, especially for the demanding needs of textileprinting. One of the surprising aspects is that both the chemicalmixture where Z₁, Z₂ and Z₃ are each present as the isocyanate reactivecomponents during the preparation of the crosslinked polyurethane andthe physical mixture of the crosslinked polyurethane produced from thediols Z₁, and Z₂ and the crosslinked polyurethane produced from thediols Z₂ and Z₃ are equally capable of producing this improved result.

Examples of polyurethanes that can be used in the crosslinkedpolyurethane dispersoids are described below. As indicated above, thecrosslinking of the polyurethanes is achieved prior to its addition tothe ink system.

Colorants

Suitable colorants for the inks of this invention include solublecolorants such as dyes, and insoluble colorants such as dispersedpigments (pigment plus dispersing agent) and self-dispersing pigments.

Conventional dyes such as anionic, cationic, amphoteric and non-ionicdyes are useful in this invention. Such dyes are well known to those ofordinary skill in the art. Anionic dyes are those dyes that, in aqueoussolution, yield colored anions. Cationic dyes are those dyes that, inaqueous solution, yield colored cations. Typically anionic dyes containcarboxylic or sulfonic acid groups as the ionic moiety. Cationic dyesusually contain quaternary nitrogen groups.

The types of anionic dyes most useful in this invention are, forexample, Acid, Direct, Food, Mordant and Reactive dyes. Anionic dyes areselected from the group consisting of nitroso compounds, nitrocompounds, azo compounds, stilbene compounds, triarylmethane compounds,xanthene compounds, quinoline compounds, thiazole compounds, azinecompounds, oxazine compounds, thiazine compounds, aminoketone compounds,anthraquinone compounds, indigoid compounds and phthalocyaninecompounds.

The types of cationic dyes that are most useful in this inventioninclude mainly the basic dyes and some of the mordant dyes that aredesigned to bind acidic sites on a substrate, such as fibers. Usefultypes of such dyes include the azo compounds, diphenylmethane compounds,triarylmethanes, xanthene compounds, acridine compounds, quinolinecompounds, methine or polymethine compounds, thiazole compounds,indamine or indophenyl compounds, azine compounds, oxazine compounds,and thiazine compounds, among others, all of which are well known tothose skilled in the art.

Useful dyes include (cyan) Acid Blue 9 and Direct Blue 199; (magenta)Acid Red 52, Reactive Red 180, Acid Red 37, CI Reactive Red 23; and(yellow) Direct Yellow 86, Direct Yellow 132 and Acid Yellow 23.

Pigments suitable for use in the present invention are those generallywell-known in the art for aqueous inkjet inks. Traditionally, pigmentsare stabilized by dispersing agents, such as polymeric dispersants orsurfactants, to produce a stable dispersion of the pigment in thevehicle. More recently though, so-called “self-dispersible” or“self-dispersing” pigments (hereafter “SDP”) have been developed. As thename would imply, SDPs are dispersible in water without dispersants.Dispersed dyes are also considered pigments as they are insoluble in theaqueous inks used herein.

Pigments that are stabilized by added dispersing agents may be preparedby methods known in the art. It is generally desirable to make thestabilized pigment in a concentrated form. The stabilized pigment isfirst prepared by premixing the selected pigment(s) and polymericdispersant(s) in an aqueous carrier medium (such as water and,optionally, a water-miscible solvent), and then dispersing ordeflocculating the pigment. The dispersing step may be accomplished in a2-roll mill, media mill, a horizontal mini mill, a ball mill, anattritor, or by passing the mixture through a plurality of nozzleswithin a liquid jet interaction chamber at a liquid pressure of at least5,000 psi to produce a uniform dispersion of the pigment particles inthe aqueous carrier medium (microfluidizer). Alternatively, theconcentrates may be prepared by dry milling the polymeric dispersant andthe pigment under pressure. After the milling process is complete thepigment concentrate may be “let down” into an aqueous system. “Let down”refers to the dilution of the concentrate with mixing or dispersing, theintensity of the mixing/dispersing normally being determined by trialand error using routine methodology, and often being dependent on thecombination of the polymeric dispersant, solvent and pigment.

The dispersant used to stabilize the pigment is preferably a polymericdispersant. Either structured or random polymers may be used, althoughstructured polymers are preferred for use as dispersants for reasonswell known in the art. The term “structured polymer” means polymershaving a block, branched or graft structure. Examples of structuredpolymers include AB or BAB block copolymers such as those disclosed inU.S. Pat. No. 5,085,698; ABC block copolymers such as those disclosed inEP-A-0556649; and graft polymers such as those disclosed in U.S. Pat.No. 5,231,131. Other polymeric dispersants that can be used aredescribed, for example, in U.S. Pat. No. 6,117,921, U.S. Pat. No.6,262,152, U.S. Pat. No. 6,306,994, U.S. Pat. No. 6,433,117, andco-owned and co-pending U.S. Provisional Patent Application 61/005,977(filed Dec. 10, 2007).

Polymer dispersants suitable for use in the present invention generallycomprise both hydrophobic and hydrophilic monomers. Some examples ofhydrophobic monomers used in random polymers are methyl methacrylate,n-butyl methacrylate, 2-ethylhexyl methacrylate, benzyl methacrylate,2-phenylethyl methacrylate and the corresponding acrylates. Examples ofhydrophilic monomers are methacrylic acid, acrylic acid,dimethylaminoethyl(meth)acrylate and salts thereof. Also quaternarysalts of dimethylaminoethyl(meth)acrylate may be employed.

A wide variety of organic and inorganic pigments, alone or incombination, may be selected to make the ink. The term “pigment” as usedherein means an insoluble colorant. The pigment particles aresufficiently small to permit free flow of the ink through the inkjetprinting device, especially at the ejecting nozzles that usually have adiameter ranging from about 10 micron to about 50 micron. The particlesize also has an influence on the pigment dispersion stability, which iscritical throughout the life of the ink. Brownian motion of minuteparticles will help prevent the particles from flocculation. It is alsodesirable to use small particles for maximum color strength and gloss.The range of useful particle size is typically about 0.005 micron toabout 15 micron. Preferably, the pigment particle size should range fromabout 0.005 to about 5 micron and, most preferably, from about 0.005 toabout 1 micron. The average particle size as measured by dynamic lightscattering is preferably less than about 500 nm, more preferably lessthan about 300 nm.

The selected pigment(s) may be used in dry or wet form. For example,pigments are usually manufactured in aqueous media and the resultingpigment is obtained as water-wet presscake. In presscake form, thepigment is not agglomerated to the extent that it is in dry form. Thus,pigments in water-wet presscake form do not require as muchdeflocculation in the process of preparing the inks as pigments in dryform. Representative commercial dry pigments are listed in previouslydescribed U.S. Pat. No. 5,085,698.

In the case of organic pigments, the ink may contain up to about 30%,preferably about 0.1 to about 25%, and more preferably about 0.25 toabout 10%, pigment by weight based on the total ink weight. If aninorganic pigment is selected, the ink will tend to contain higherweight percentages of pigment than with comparable inks employingorganic pigment, and may be as high as about 75% in some cases, sinceinorganic pigments generally have higher specific gravities than organicpigments.

Self-dispersed pigments (SDPs) can be use with the crosslinkedpolyurethane dispersoids and are often advantageous over traditionaldispersant-stabilized pigments from the standpoint of greater stabilityand lower viscosity at the same pigment loading. This can providegreater formulation latitude in final ink.

SDPs, and particularly self-dispersing carbon black pigments, aredisclosed in, for example, U.S. Pat. No. 2,439,442, U.S. Pat. No.3,023,118, U.S. Pat. No. 3,279,935 and U.S. Pat. No. 3,347,632.Additional disclosures of SDPs, methods of making SDPs and/or aqueousinkjet inks formulated with SDP's can be found in, for example, U.S.Pat. No. 5,554,739, U.S. Pat. No. 6,852,156. The preferred colorants arepigments, which include self-dispersed pigments.

Polyurethane Dispersoid Binders (PUDs)

As indicated above, a crosslinked polyurethane dispersoid refers to anaqueous dispersion of a polymer containing urethane groups andcrosslinking, as those terms are understood by persons of ordinary skillin the art. These crosslinked polyurethane dispersoid require thepresence of each of diols, Z₁, Z₂ and Z₃, in the polyurethane orphysical mixtures of the diols taken two at a time, Z₁ and Z₂ and Z₂ andZ₃. in the polyurethane. It will be recognized that the crosslinkedpolyurethanes are prepared in a manner such that in the former case allthree of the diols are present in the polyurethane, however there may besome that have only two of the three diols because of variability in thechemistries.

These polymers incorporate hydrophilic functionality to the extentrequired to maintain a stable dispersion of the polymer in water and,more preferably, the aqueous vehicle and the main source of thehydrophilic functionality is from the diol, Z₂. The main advantage ofincorporating hydrophilic functionality into the polymer is thatdispersion can be performed with minimal energy so that the dispersingprocesses do not require strong shear forces, resulting in finerparticle size, better dispersion stability, and reduced watersensitivity of the polymers obtained after evaporation of the water.These polymers must incorporate ionic and may incorporate additionalnonionic functionality to the extent required to maintain a stabledispersion of the polymer in water.

In general, the dispersion stability of the crosslinked polyurethane inthe aqueous vehicle is achieved by incorporating ionic components in thepolyurethane polymer, which facilitates stabilizing the crosslinkedpolyurethane in aqueous systems. This dispersion stability means thepolyurethane will not phase separate, coagulate, and/or precipitate fromthe aqueous system.

Examples of suitable polyurethanes are those in which the polymer ispredominantly stabilized in the dispersion through incorporated anionicfunctionality, and an example of this is anionic functionality such asneutralized acid groups (“anionically stabilized polyurethanedispersoid”). In general, the preferred anionic compound is the diol Z₂.

The diols, Z₁, Z₂ and Z₃, in the polyurethane or physical mixtures ofthe diols taken two at a time, Z₁ and Z₂ and Z₂ and Z₃ in thepolyurethane provide polyurethane binders with improved hydrolyticstability. The improved hydrolytic stability is required because manypolyurethanes hydrolyze in their own aqueous dispersion or in the inkwhich contains the polyurethane.

A way to measure this hydrolytic stability is to draw down a freshlymade polyurethane into a film, dry the film, weigh a portion of the filmwhich is suspended in an aqueous solution for a fixed time. Aftersoaking in water the polyurethane is wiped dry and weighed; the weightgain is attributed to absorbed water. The change in weight is calculateand labeled as % water uptake. A comparison is made by doing the samesteps with a polyurethane after it has been heated to 70° C. for 7 days.Improved inventive polyurethanes are characterized by showing similar oronly modest water uptake of the as made polyurethane and the heat agedpolyurethane.

Suitable aqueous polyurethane dispersoids are typically prepared bymulti-step synthetic processes in which an NCO terminated prepolymer isformed, this prepolymer is added to water or water is added to theprepolymer forming a polymer dispersed in water (aqueous dispersion) andsubsequently chain extended in the aqueous phase. The prepolymer can beformed by a single or multi-step process. Chain extension, if used, canalso be a single or multi-step process. The important crosslinking canoccur as part of these single or multi-step processes. It is preferredthat the crosslinking for the polyurethane is completed prior to itsaddition to the ink formulation. The polyurethane synthesis and thecrosslinking is completed prior to any mixing with other components andthus the colorants and the crosslinked polyurethane are completelyindependent.

After the polyurethane dispersoid is prepared it is included with theother ink components to produce the inkjet ink. The details of thepreparation of the ink are familiar to those skilled in the art.

As indicated above, the polyurethane dispersoid is typically prepared bya multiple step process. Typically, in the first stage of prepolymerformation, a diisocyanate is reacted with a compound, polymer, ormixtures of compound, mixture of polymers or a mixture thereof, eachcontaining two NCO-reactive groups. An additional compound or compounds,all containing ≧2 NCO-reactive groups as well as a stabilizing ionicfunctionality, is also used to form an intermediate polymer. Thisintermediate polymer or pre-polymer can be terminated with either anNCO-group or a NCO-reactive group. The terminal groups are defined bythe molar ratio of NCO to NCO-reactive groups in the prepolymer stage.Typically, the pre-polymer is an NCO-terminated material that isachieved by using a molar excess of NCO. Thus, the molar ratio ofdiisocyanate to compounds containing two isocyanate-reactive groups isat least about 1.1:1.0, preferably about 1.20:1.0 to about 5.0:1.0, andmore preferably about 1.20:1.0 to about 2.5:1.0. In general, the ratiosare achieved by preparing, in a first stage, an NCO-terminatedintermediate by reacting one of the NCO-reactive compounds, having atleast 2 NCO reactive groups, with all or part of the diisocyanate. Thisis followed, in sequence, by additions of other NCO-reactive compounds,if desired. When all reactions are complete the group, NCO and/orNCO-reactive groups will be found at the termini of the pre-polymer.These components are reacted in amounts sufficient to provide a molarratio such that the overall equivalent ratio of NCO groups toNCO-reactive groups is achieved.

The means to achieve the crosslinking of the polyurethane generallyrelies on at least one component of the polyurethane (starting materialand/or intermediate) having 3 or more functional reaction sites.Reaction of each of the 3 (or more) reaction sites will produce acrosslinked polyurethane (3-dimensional matrix). When only two reactivesites are available on each reactive components, only linear (albeitpossibly high molecular weight) polyurethanes can be produced. Examplesof crosslinking techniques include but are not limited to the following:

the isocyanate-reactive moiety has at least 3 reactive groups, forexample polyfunctional amines or polyol;

the isocyanate has at least 3 isocyanate groups;

the prepolymer chain has at least 3 reactive sites that can react viareactions other than the isocyanate reaction, for example with aminotrialkoxysilanes;

addition of a reactive component with at least 3 reactive sites to thepolyurethane prior to its use in the inkjet ink preparations, forexample tri-functional epoxy crosslinkers;

addition of a water-dispersible crosslinker with oxazolinefunctionality;

synthesis of a polyurethane with carbonyl functionality, followed byaddition of a dihydrazide compound;

and any combination of the these crosslinking methods and othercrosslinking means known to those of ordinary skill in the relevant art.

Also, it is understood that these crosslinking components may only be a(small) fraction of the total reactive functionality added to thepolyurethane. For example, when polyfunctional amines are added, mono-and difunctional amines may also be present for reaction with theisocyanates. The polyfunctional amine may be a minor portion of theamines.

The crosslinking preferably occurs during the preparation of thepolyurethane. A preferred time for the crosslinking in the polyurethanereaction sequence would be just prior to, at, or after the time of theinversion step. That is, crosslinking preferably occurs during theaddition of water to the polyurethane preparation mixture or shortlythereafter. The inversion is that point where sufficient water is addedsuch that the polyurethane is converted to its stable dispersed aqueousform. Most preferred is that the crosslinking occurs after theinversion. Furthermore, all of the crosslinking of the polyurethane ispreferably complete prior to its incorporation into the ink formulation.

Alternatively, the crosslinking can occur during the initial formationof the urethane bonds when the isocyanates or isocyanate-reactive groupshave 3 or more groups capable of reacting. If the crosslinking is doneat this early stage, the extent of crosslinking must not lead to gelformation. Too much crosslinking at this stage will prevent theformation of a stable polyurethane dispersion.

The amount of crosslinking of the polyurethane to achieve the desiredinkjet ink for printing on different substrates can vary over a broadrange. A preferred use of these inks is for the printing of textiles.While not being bound to theory, the amount of crosslinking is afunction of the polyurethane composition, the whole sequence of reactionconditions utilized to form the polyurethane and other factors known tothose of ordinary skill in the art. The extent of crosslinking, theinkjet ink formulation, the colorant, other inks in the inkjet set, thetextile, the post treatment exposure to heat and/or pressure, and theprinting technique for the textile, all contribute to the final printedtextile performance. For the printing technique this can include pre andpost treatment of the textile.

Based on techniques described herein, a person of ordinary skilled inthe art is able to determine, via routine experimentation, thecrosslinking needed for a particularly type of polyurethane to obtain aneffective inkjet ink for textiles. Furthermore, as indicated above,these inks may also be used for plain paper, photo paper,transparencies, vinyl and other printable substrates.

The amount of crosslinking can be measured by a standard tetrahydrofuraninsolubles test. For the purposes of definition herein, thetetrahydrofuran (THF) insolubles of the polyurethane dispersoid ismeasured by mixing 1 gram of the polyurethane dispersoid with 30 gramsof THF in a pre-weighed centrifuge tube. After the solution iscentrifuged for 2 hours at 17,000 rpm, the top liquid layer is pouredout and the non-dissolved gel in the bottom is left. The centrifuge tubewith the non-dissolved gel is re-weighed after the tube is put in theoven and dried for 2 hours at 110° C. The following equation is thenused to calculate the result:

% THF insolubles of polyurethane=(weight of tube and non-dissolvedgel−weight of tube)/(sample weight*polyurethane solid %). The % THFinsolubles of polyurethane is reported as a weight percent based on thedry polymer.

The upper limit of crosslinking is related to the ability to make astable aqueous polyurethane dispersion. If a highly crosslinkedpolyurethane has adequate ionic or non-ionic functionality such that itis a stable when inverted into water, then its level of crosslinkingwill lead to an improved inkjet ink for textiles. The upper limit ofcrosslinking as measured by the THF insolubles test is about 50%. Thelower limit of crosslinking in the polyurethane dispersoid is about 1%or greater, preferably about 2% or greater, as measured by the THFinsolubles test.

Another way of measuring the insolubles derived from the crosslinking isto use swell ratio test that is used for testing coatings. Thepolyurethane dispersion is drawn down into film of defined thickness.Then a circular piece of the film is cut out and its dimensionsobserved. Then a drop of a solvent such as methylene chloride, THF isput on the piece of the film. Films with no crosslinking will likelydissolve under these conditions, and films with varying degrees ofcrosslinking can be correlated with dimensional changes.

An alternative way to achieve an effective amount of crosslinking in thepolyurethane is to choose a polyurethane that has crosslinkable sites,then crosslink those sites via self-crosslinking and/or addedcrosslinking agents. Examples of self-crosslinking functionalityincludes, for example, silyl functionality (self-condensing) availablefrom certain starting materials as indicated above, as well ascombinations of reactive functionalities incorporated into thepolyurethanes, such as epoxy/hydroxyl, epoxy/acid andisocyanate/hydroxyl. Examples of polyurethanes and complementarycrosslinking agents include: (1) a polyurethane with isocyanate reactivesites (such as hydroxyl and/or amine groups) and an isocyanatecrosslinking reactant, and (2) a polyurethane with unreacted isocyanategroups and an isocyanate-reactive crosslinking reactant (containing, forexample, hydroxyl and/or amine groups). The complementary reactant canbe added to the polyurethane, such that crosslinking is done prior toits incorporation into an ink formulation. The crosslinking shouldpreferably be substantially completed prior to the incorporation of thedispersoid into the ink formulation. This crosslinked polyurethanepreferably has from about 1% to about 50% crosslinking as measured bythe THF insolubles test.

Combinations of two or more polyurethane crosslinked dispersoid bindersmay also be utilized in the formulation of the ink. Combinations of thesecond crosslinked dispersoid polyurethane with diols Z₁ and Z₂ andthird crosslinked dispersoid polyurethanes with diols Z₂ and Z₃ areexamples of the instant invention. The crosslinked polyurethanedispersoid can be mixed with other binders, including latexes, and thelike. A non-limiting list of these binders includes dispersed acrylics,neoprenes, dispersed nylons, and non-crosslinked polyurethanesdispersions which would have no insoluble fraction as detected by theTHF insolubles test.

The crosslinked polyurethane dispersoid contain diols where each of Z₁,Z₂ and Z₃, are present in the polyurethane or physical mixtures of thediols taken two at a time, Z₁ and Z₂ and Z₂ and Z₃ are present.

Diol Z₁ is a polyether diol shown in Structure (I) and are oligomers andpolymers in which at least 50% of the repeating units have 3 to 36methylene groups in the ether chemical groups. More preferably fromabout 75% to 100%, still more preferably from about 90% to 100%, andeven more preferably from about 99% to 100%, of the repeating units are3 to 36 methylene groups in the ether chemical groups (in Structure (I)m=3-36). The preferable number of methylene groups are from 3 to 12 andmore preferably 3 or 4. The polyether diol shown in Structure (I) can beprepared by polycondensation of monomers comprising alpha, omega diolswhere m=3-36, thus resulting in polymers or copolymers containing thestructural linkage shown above. As indicated above, at least 50% of therepeating units are 3 to 36 methylene ether units.

The oligomers and polymers based on the polyether diol shown inStructure (I), have from 2 to about 50 of the ether diol repeatinggroups shown in Structure (I); more preferable about 5 to about 20 ofthe ether diol repeating groups shown in Structure (I), where p denotesthe number of repeating groups. In structure (I) R₅ and R₆ are hydrogen,alkyl, substituted alkyl, aryl; where the R₅ and R₆ are the same ordifferent with each substituted methylene group and where R₅ and R₆ canbe joined to form a cyclic structure. The substituted alkyl grouppreferably does not contain isocyanate reactive groups except asdescribed below where a limited amount of trihydric alcohols can beallowed. In general, the substituted alkyls are intended to be inertduring the polyurethane preparation.

In addition to the preferably 3 to 12 methylene ether units, lesseramounts of other units, such as other polyalkylene ether repeating unitsderived from ethylene oxide and propylene oxide may be present. Theamount of the ethylene glycols and 1.2-propylene glycols which arederived from epoxides such as ethylene oxide, propylene oxide, butyleneoxide, etc are limited to less than 10% of the total polyether diolweight.

Diol Z₃ is selected from polycarbonate diols, polyamide diols andpoly(meth) acrylate diols.

Polycarbonates containing hydroxyl groups include those known, per se,such as the products obtained from the reaction of diols such aspropanediol-(1,3), butanediol-(1,4) and/or hexanediol-(1,6), diethyleneglycol, triethylene glycol or tetraethylene glycol, higher polyetherdiols with phosgene, diarylcarbonates such as diphenylcarbonate,dialkylcarbonates such as diethylcarbonate or with cyclic carbonatessuch as ethylene or propylene carbonate.

Polycarbonate diols for blending are preferably selected from the groupconsisting of polyethylene carbonate diol, polytrimethylene carbonatediol, polybutylene carbonate diol and polyhexylene carbonate.

Polyamide polyols include those products obtained by reacting i) anorganic compound selected from the group consisting of aromatic,aliphatic, and cycloaliphatic anhydrides and diacid halides, with ii) anamine containing compound including amino alcohols, diamines andmixtures thereof,

The compound (i), used to form the polyamide is preferably acycloaliphatic anhydride or a diacid halide. Examples of these include,but are not limited to 1,2-cyclohexane dicarboxylic anhydride, phthalicanhydride or succinic anhydride, or a diacid halide such asterephthaloyl chloride, succinyl chloride or adipoyl chloride. The aminecontaining compound (ii), used to form the polyamide includes primaryand secondary amino alcohols, or diamines. Examples of suitable aminoalcohols include, but are not limited to ethanolamine, propanol amine,2-amino-2-methyl-1-propanol and diethanol amine. Diamines includediaminocyclohexane and ethylene diamine.

The polyamide formed by the reaction of compounds (i) and (ii) isformulated to provide a polyamide having hydroxyl substituted reactivetermini. If diamine is used as the amine containing compound, theproduct is subsequently reacted with excess amino alcohol to provide apolyamide substituted at its reactive termini with hydroxyl groups.Thiol terminated polyamides are prepared by the same process bysubstituting amino thiols for the amino alcohol.

Poly(meth)acrylates containing hydroxyl groups include those common inthe art of addition polymerization such as cationic, anionic and radicalpolymerization and the like. Examples are alpha-omega diols. An exampleof these type of diols are those which are prepared by a “living” or“control” or chain transfer polymerization processes which enables theplacement of one hydroxyl group at or near the termini of the polymer.U.S. Pat. No. 6,248,839 and U.S. Pat. No. 5,990,245 have examples ofprotocol for making terminal diols. Other di-NCO reactivepoly(meth)acrylate terminal polymers can be used. An example would beend groups other than hydroxyl such as amino or thiol, and may alsoinclude mixed end groups with hydroxyl.

Diol, Z₂ is an isocyanate-reactive compound containing ionic (i.e.,ionizable) groups. For example, anionic and cationic groups can bechemically incorporated into the polyurethane to provide hydrophilicityand enable the polyurethane to be dispersed in an aqueous medium.

Examples of ionic dispersing groups include carboxylate groups (—COOM),phosphate groups (—OPO₃ M₂), phosphonate groups (—PO₃ M₂), sulfonategroups (—SO₃ M), quaternary ammonium groups (—NR₃Y, wherein Y is amonovalent anion such as chlorine or hydroxyl), or any other effectiveionic group. M is a cation such as a monovalent metal ion (e.g., Na⁺,K⁺, Li⁺, etc.), H⁺, NR₄ ⁺, and each R can be independently an alkyl,aralkyl, aryl, or hydrogen. These ionic dispersing groups are typicallylocated pendant from the polyurethane backbone.

In the case of anionic group substitution, the groups can be carboxylicacid groups, carboxylate groups, sulphonic acid groups, sulphonategroups, phosphoric acid groups and phosphonate groups, The acid saltsare formed by neutralizing the corresponding acid groups either priorto, during or after formation of the NCO prepolymer, preferably afterformation of the NCO prepolymer.

Suitable compounds for incorporating carboxyl groups are described inU.S. Pat. No. 3,479,310, U.S. Pat. No. 4,108,814 and U.S. Pat. No.4,408,008. The neutralizing agents for converting the carboxylic acidgroups to carboxylate salt groups are described in the precedingpublications, and are also discussed hereinafter. Within the context ofthis invention, the term “neutralizing agents” is meant to embrace alltypes of agents that are useful for converting carboxylic acid groups tothe more hydrophilic carboxylate salt groups. In like manner, sulphonicacid groups, sulphonate groups, phosphoric acid groups, and phosphonategroups can be neutralized with similar compounds to their morehydrophilic salt form.

Examples of carboxylic group-containing compounds are thehydroxy-carboxylic acids corresponding to the formula (HO)xQ(COOH)ywherein Q represents a straight or branched, hydrocarbon radicalcontaining 1 to 12 carbon atoms, x is 1 or 2 (preferably 2), and y is 1to 3 (preferably 1 or 2).

Examples of these hydroxy-carboxylic acids include citric acid, tartaricacid and hydroxypivalic acid.Especially preferred acids are those of the above-mentioned formulawherein x=2 and y=1. These dihydroxy alkanoic acids are described inU.S. Pat. No. 3,412,054. Especially preferred dihydroxy alkanoic acidsare the alpha,alpha-dimethylol alkanoic acids represented by thestructural formula:

wherein Q′ is hydrogen or an alkyl group containing 1 to 8 carbon atoms.The most preferred compound is alpha,alpha-dimethylol propionic acid,i.e., wherein Q′ is methyl in the above formula.

When the ionic stabilizing groups are acids, the acid groups areincorporated in an amount sufficient to provide an acid group content,known by those skilled in the art as acid number (mg KOH per gram solidpolymer), of at least about 5, preferably at least about 10 milligramsKOH per 1.0 gram of polyurethane. The upper limit for the acid number(AN) is about 50, preferably about 40.

For the first crosslinked polyurethane where Z₁, Z₂, and Z₃ are eachpresent, the molar amount of Z₂ must be sufficient to provide thedispersion stability as described above. In addition, Z₁, and Z₃ shouldbe present in the mole ratio of about 1:1 to about 1:10, preferablyabout 1:1.5 to about 1:7.

For the case where the second and third crosslinked polyurethane arepresent, the molar amount of Z₂ must be sufficient to provide thedispersion stability as described above. In addition, Z₁, of the secondcrosslinked polyurethane and Z₃ third crosslinked polyurethane should bepresent in the mole ratio of about 1:1 to about 1:10, preferably about1:1.5 to about 1:7.

The preferred ratios of Z₁, Z₂, and Z₃ are chosen to obtain the desiredimproved hydrolysis stability of the polyurethanes, improvedwashfastness, while preserving other attributes such as hand, crock ofthe printed textiles.

Suitable diisocyanates are those that contain either aromatic,cycloaliphatic or aliphatic groups bound to the isocyanate groups.Mixtures of these compounds may also be used. The preferred is aprepolymer that has isocyanates bound to a cycloaliphatic or aliphaticmoieties. If aromatic diisocyanates are used, cycloaliphatic oraliphatic isocyanates are preferably present as well.

Examples of suitable diisocyanates include cyclohexane-1,3- and-1,4-diisocyanate;1-isocyanato-3-isocyanatomethyl-3,5,5-trimethyl-cyclohexane (isophoronediisocyanate or IPDI); bis-(4-isocyanatocyclohexyl)-methane; 1,3- and1,4-bis-(isocyanatomethyl)-cyclohexane; 1-isocyanato-2-isocyanatomethylcyclopentane; 2,4′-diisocyanato-dicyclohexyl methane;bis-(4-isocyanato-3-methyl-cyclohexyl)-methane,alpha,alpha,alpha′,alpha′-tetramethyl-1,3- and/or -1,4-xylylenediisocyanate; 1-isocyanato-1-methyl-4(3)-isocyanatomethyl cyclohexane;and 2,4- and/or 2,6-hexahydrotoluoylene diisocyanate.

Additional diisocyanates may be linear or branched and contain 4 to 12carbon atoms, preferably 4 to 9 carbon which include 1,4-tetramethylenediisocyanate; 1,6-hexamethylene diisocyanate;2,2,4-trimethyl-1,6-hexamethylene diisocyanate; and 1,12-dodecamethylenediisocyanate. 1,6-hexamethylene diisocyanate and isophorone diisocyanateare examples of diisocyanates effective for the crosslinkedpolyurethanes

In addition to the above-mentioned components, which are preferablydifunctional in the isocyanate polyaddition reaction, mono-functionaland even small portions of trifunctional and higher functionalcomponents generally known in polyurethane chemistry, such astrimethylolpropane or 4-isocyanantomethyl-1,8-octamethylenediisocyanate, may be used in cases in which branching of the NCOprepolymer or polyurethane is desired. However, the NCO prepolymersshould be substantially linear and this may be achieved by maintainingthe average functionality of the prepolymer starting components at orbelow 2:1.

Process conditions for preparing the preferred NCO containingprepolymers have been discussed in the publications previously noted.The finished NCO containing prepolymer should have a isocyanate contentof about 1 to about 20%, preferably about 1 to about 10% by weight,based on the weight of prepolymer solids.

The crosslinked polyurethanes dispersoids are typical prepared by chainextending these NCO containing prepolymers. Chain extenders arepolyamine chain extenders, which can optionally be partially or whollyblocked as disclosed in U.S. Pat. No. 4,269,748 and U.S. Pat. No.4,829,122. These publications disclose the preparation of aqueouspolyurethane dispersoids by mixing NCO-containing prepolymers with atleast partially blocked, diamine or hydrazine chain extenders in theabsence of water and then adding the mixture to water. Upon contact withwater the blocking agent is released and the resulting unblockedpolyamine reacts with the NCO containing prepolymer to form thepolyurethane.

Suitable blocked amines and hydrazines include the reaction products ofpolyamines with ketones and aldehydes to form ketimines and aldimines,and the reaction of hydrazine with ketones and aldehydes to formketazines, aldazines, ketone hydrazones and aldehyde hydrazones. The atleast partially blocked polyamines contain at most one primary orsecondary amino group and at least one blocked primary or secondaryamino group which releases a free primary or secondary amino group inthe presence of water.

Suitable polyamines for preparing the at least partially blockedpolyamines have an average functionality, i.e., the number of aminenitrogens per molecule, of 2 to 6, preferably 2 to 4 and more preferably2 to 3. The desired functionalities can be obtained by using mixtures ofpolyamines containing primary or secondary amino groups. The polyaminesare generally aromatic, aliphatic or alicyclic amines and containbetween 1 to 30, preferably 2 to 15 and more preferably 2 to 10 carbonatoms. These polyamines may contain additional substituents providedthat they are not as reactive with isocyanate groups as the primary orsecondary amines. These same polyamines can be partially or whollyblocked polyamines.

A suitable method of chain extension is to add polyamine to theNCO-prepolymer before, during or after the pre-polymer inversion intowater. Optionally, the chain extension can occur after pre-polymerinversion. The polyamines include1-amino-3-aminomethyl-3,5,5-trimethylcyclohexane (isophorone diamine orIPDA), bis-(4-amino-cyclohexyl)-methane,bis-(4-amino-3-methylcyclohexyl)-methane, 1,6-diaminohexane, hydrazine,ethylene diamine, diethylene triamine, triethylene tetramine,tetraethylene pentamine and pentaethylene hexamine.

In some cases, chain termination may be desirable. This requires theaddition, in most cases, of a mono-NCO reactive material such as amono-amine or mono-alcohol. The materials can be added before, during orafter inversion of the pre-polymer. Poly-NCO reactive materials can beused where one of the NCO-reactive groups reacts substantially fasterthan the others. Examples would be ethanol amine and diethanol amine.The amine group will react much faster with the NCO group than thealcohol.

Suitable chain terminators would be amines or alcohols having an averagefunctionality per molecule of 1, i.e., the number of primary orsecondary amine nitrogens or alcohol oxygens would average 1 permolecule. The desired functionalities can be obtained by using primaryor secondary amino groups. The amines or alcohols are generallyaromatic, aliphatic or alicyclic and contain between 1 to 30, preferably2 to 15 and more preferably 2 to 10 carbon atoms. These may containadditional substituents provided that they are not as reactive withisocyanate groups as the amine or alcohol groups. Examples of chainterminators include dibutylamine, diethylamine, diisopropyle amine,bis(methoxyethyl) amine, and other amines.

Chain terminators and chain extenders can be used together, either asmixtures or as sequential additions to the NCO-prepolymer.

The amount of chain extender and/or chain terminator to be used inaccordance with the present invention is dependent upon the number ofisocyanate groups in the prepolymer. Preferably, the ratio of isocyanategroups of the prepolymer to isocyanate-reactive groups of the chainextender/terminator is between about 1.0:0.6 and about 1.0:1.1, morepreferably between about 1.0:0.7 and about 1.0:1.1, on an equivalentbasis. Any isocyanate groups that are not chain extended/terminated withan amine or alcohol will react with water, which functions as a chainextender.

Chain extension can take place prior to addition of water in theprocess, but typically takes place by combining the NCO containingprepolymer, chain extender, water and other optional components underagitation.

In order to have a stable dispersion, a sufficient amount of the ionicgroups (if present) must be neutralized so that, when combined with theoptional hydrophilic ethylene oxide and other alkenyl oxide units andoptional external emulsifiers, the resulting polyurethane will remainstably dispersed in the aqueous medium. Generally, at least about 70%,preferably at least about 80%, of the acid groups are neutralized to thecorresponding carboxylate salt groups. Alternatively, cationic groups inthe polyurethane can be quaternary ammonium groups (—NR3Y, wherein Y isa monovalent anion such as chlorine or hydroxyl).

Suitable neutralizing agents for converting the acid groups to saltgroups include tertiary amines, alkali metal cations and ammonia.Examples of these neutralizing agents are disclosed in U.S. Pat. No.4,701,480, as well as U.S. Pat. No. 4,501,852. Preferred neutralizingagents are the trialkyl-substituted tertiary amines, such as triethylamine, tripropyl amine, dimethylcyclohexyl amine, and dimethylethylamine. Substituted amines are also useful neutralizing groups such asdiethyl ethanol amine or diethanol methyl amine.

Neutralization may take place at any point in the process. Typicalprocedures include at least some neutralization of the prepolymer, whichis then chain extended/terminated in water in the presence of additionalneutralizing agent.

The final product is a stable aqueous dispersoid of polyurethaneparticles having a dry polymer solids content of up to about 60% byweight, preferably about 15 to about 60% by weight and most preferablyabout 30 to about 40% by weight. The solid content is also called asolids basis. When the crosslinked polyurethane dispersoid amount isreported in the inks, it is reported as weight of the crosslinkedpolyurethane dispersoid as the dry polymer. If the polyurethane is theaqueous is weight 35% then an ink with 7% crosslinked polyurethanedispersoid binder (as the dry polymer solids) would have 20 parts byweight added of the aqueous crosslinked polyurethane dispersion.However, it is always possible to dilute the dispersions to any minimumsolids content desired. The dispersion of crosslinked polyurethanedispersoid is an offwhite milky looking substance typical of these typesof dispersions; there can be some yellowness which is likely developedfrom heating organic materials over extended time periods.

Other additives to the inkjet ink may be include post printing curingagents that can undergo post printing curing after the ink isformulated. This additional curing for the purposes of this applicationis called post printing curing at the time of the printing, or posttreatment of the printed material. The crosslinking in the crosslinkedpolyurethane dispersoid as measured by the THF insolubles test isindependent of any post curing. The crosslinked polyurethane dispersoidmay or may not participate in the post printing curing.

Post printing curing agents if added to the ink will lead to anadditional post printing curing treatment after the image is printed.This additional post printing curing is often facilitated by heating ofthe sample after it is printed. An example of a post printing curingagent would be the addition of a melamine to the ink. After printing theink with the melamine, it would be heated to affect post printing curingat or to the substrate.

Example of suitable post printing curing agents include amide andamine-formaldehyde resin, phenolic resins, urea resins and blockedpolyisocyanate. The selected post printing curing agent is soluble ordispersible in the ink. Inks contain the crosslinked hydrolyticallystable polyurethane PUD binder and the selected post printing curing arestable in storage which means no curing reaction took place beforeprinting. Only after the ink is printed and when the printed image isfused with heat and optionally pressure, the post printing curingundergoes chemical reaction with the one or more of the polyurethanedispersoid, dispersant, hydroxyl functional ink vehicle, the textilesubstrate, etc. Melamine-formaldehyde resin is preferred and an exampleof this is Cymel® 303 ULF, from Cytec, West Patterson N.J. The postprinting curing agent loading in the ink could range from 0.2 to about12%, preferably from about 1 to about 8%. And optionally 0.01% to 1%acid or acid blocked catalyst could be used to further increase postprinting curing efficiency. An example of acid catalysts include Nacure®3525 from King Industries, Norwalk Conn. An example of this is theaddition of a melamine to the ink. After printing the ink with themelamine, it is heated to affect further post printing curing at or ontothe substrate. Textiles are a preferred substrate for this post printingcuring.

Aqueous Vehicle

“Aqueous vehicle” refers to water or a mixture of water and at least onewater-soluble organic solvent (co-solvent). Selection of a suitablemixture depends on requirements of the specific application, such asdesired surface tension and viscosity, the selected colorant, dryingtime of the ink, and the type of substrate onto which the ink will beprinted. Representative examples of water-soluble organic solvents thatmay be selected are disclosed in U.S. Pat. No. 5,085,698.

The aqueous inks of the present invention are comprised primarily ofwater. Thus, the instant inks comprise at least about 40%, preferably atleast about 45%, and more preferably at least about 50% by weight ofwater, based on the total weight of the ink.

If a mixture of water and a water-soluble solvent is used, the aqueousvehicle typically will contain about 40% to about 95% by weight waterwith the balance (i.e., about 60% to about 5% by weight) being thewater-soluble solvent. Preferred compositions contain about 65% to about95% by weight water, based on the total weight of the aqueous vehicle.

The amount of aqueous vehicle in the ink is typically in the range ofabout 70% to about 99.8%, and preferably about 80% to about 99.8%, byweight based on total weight of the ink.

The aqueous vehicle can be made to be fast penetrating (rapid drying) byincluding surfactants or penetrating agents such as glycol ethers and1,2-alkanediols. Glycol ethers include ethylene glycol monobutyl ether,diethylene glycol mono-n-propyl ether, ethylene glycol mono-iso-propylether, diethylene glycol mono-iso-propyl ether, ethylene glycolmono-n-butyl ether, ethylene glycol mono-t-butyl ether, diethyleneglycol mono-n-butyl ether, triethylene glycol mono-n-butyl ether,diethylene glycol mono-t-butyl ether, 1-methyl-1-methoxybutanol,propylene glycol mono-t-butyl ether, propylene glycol mono-n-propylether, propylene glycol mono-iso-propyl ether, propylene glycolmono-n-butyl ether, dipropylene glycol mono-n-butyl ether, dipropyleneglycol mono-n-propyl ether, and dipropylene glycol mono-isopropyl ether.1,2-alkanediols are preferably 1,2-C₄₋₆ alkanediols, most preferably1,2-hexanediol. Suitable surfactants include ethoxylated acetylene diols(e.g. Surfynols® series from Air Products), ethoxylated primary (e.g.Neodol® series from Shell) and secondary (e.g. Tergitol® series fromUnion Carbide) alcohols, Pluronic® block copolymer surfactants,sulfosuccinates (e.g. Aerosol® series from Cytec), organosilicones (e.g.Silwet® series from Witco) and fluoro surfactants (e.g. Zonyl® seriesfrom DuPont).

The amount of glycol ether(s) and 1,2-alkanediol(s) added must beproperly determined, but is typically in the range of from about 1 toabout 15% by weight and more typically about 2 to about 10% by weight,based on the total weight of the ink.

Surfactants may be used, typically in the amount of about 0.01 to about5% and preferably about 0.1 to about 1%, based on the total weight ofthe ink.

In addition, solvents that are not water miscible may be added to theink to facilitate the printing the ink which has a polyurethanedispersoid binder in it. While not being bound by theory, it is believedthat this added non-aqueous solvent assists in the coalescence of thepolyurethane onto the printed substrate, especially a fabric in the caseof textile printing. Examples of these water-immiscible solvents arepropylene carbonate and dipropylene glycol monomethyl ether.

Proportion of Main Ingredients

The colorant levels employed in the textile inks are those levels whichare typically needed to impart the desired color density to the printedimage. Typically, for the preferred colorant the pigment is present at alevel of about 0.1% up to a level of about 30% by weight of the totalweight of ink. Alternatively, the pigment can be about 0.25 to about 25%of the total weight of the ink. Further, the pigment can be about 0.25to about 15% of the total weight of the ink.

The crosslinked polyurethane dispersoid level employed is dictated bythe range of ink properties that can be tolerated. Generally,polyurethane levels will range up to about 30%, more particularly fromabout 1% up to about 25%, and typically about 4% to about 20%, by weight(polyurethane solids basis) of the total weight of ink. Effective levelsof polyurethane are typically those where the weight ratio ofpolyurethane (solids) to colorant (pigment) is at least about 0.2,preferably more than about 0.75, alternatively more than about 1.0. Thisweight ratio must be balanced against other ink properties, such asviscosity, to maintain acceptable jetting performance. The right balanceof properties must be determined for each circumstance, which can bedone by the person of ordinary skill in the art using routineexperimentation.

Other Ingredients

The inkjet ink may contain other ingredients as are well known in theart. For example, anionic, nonionic, cationic or amphoteric surfactantsmay be used. In aqueous inks, the surfactants are typically present inthe amount of about 0.01 to about 5%, and preferably about 0.2 to about2%, based on the total weight of the ink.

Co-solvents, such as those exemplified in U.S. Pat. No. 5,272,201 may beincluded to improve pluggage inhibition properties of the inkcomposition.

Biocides may be used to inhibit growth of microorganisms.

Sequestering agents such as EDTA may also be included to eliminatedeleterious effects of heavy metal impurities.

Ink Properties

Jet velocity, separation length of the droplets, drop size and streamstability are greatly affected by the surface tension and the viscosityof the ink. Inkjet inks suitable for use with inkjet printing systemsshould have a surface tension in the range of about 20 dyne/cm to about70 dyne/cm, more preferably about 25 to about 40 dyne/cm at 25° C.Viscosity is preferably in the range of about 1 cP to about 30 cP, morepreferably about 2 to about 20 cP at 25° C. The ink has physicalproperties compatible with a wide range of ejecting conditions, i.e.,driving frequency of the pen and the shape and size of the nozzle.

The inks should have excellent storage stability for long periods.Preferably, the instant inks can sustain elevated temperature in aclosed container for extended periods (e.g. 70° C. for 7 days) withoutsubstantial increase in viscosity or particle size.

Further, the ink should not corrode parts of the inkjet printing deviceit comes in contact with, and it should be essentially odorless andnon-toxic.

Inks of the instant invention can achieve the beneficial durableproperties of washfastness.

Ink Sets

The ink sets in accordance with the present invention preferablycomprise at least three differently colored inks (such as CMY), andpreferably at least four differently colored inks (such as CMYK),wherein at least one of the inks is an aqueous inkjet ink comprising anaqueous vehicle, a colorant and a crosslinked polyurethanedispersoid(s), wherein the colorant is soluble or dispersible in theaqueous vehicle.

The ink set may further comprise one or more “gamut-expanding” inks,including different colored inks such as an orange ink, a green ink, ared ink and/or a blue ink, and combinations of full strength and lightstrengths inks such as light cyan and light magenta. These“gamut-expanding” inks are particularly useful in textile printing forsimulating the color gamut of analog screen printing, such as disclosedin US20030128246.

Method of Printing

The inks and ink sets of the present invention can be by printing withany inkjet printer. The substrate can be any suitable substrateincluding plain paper (such as standard elecrophotographic papers),treated paper (such as coated papers like photographic papers), textile,and non-porous substrates including polymeric films such as polyvinylchloride and polyester.

A particularly preferred use of the inks and ink sets of the presentinvention is in the inkjet printing of textiles. Textiles include butare not limited to cotton, wool, silk, nylon, polyester and the like,and blends thereof. The finished form of the textile includes, but isnot limited to, fabrics, garments, t-shirts furnishings such as carpetsand upholstery fabrics, and the like. Additionally, fibrous textilematerials that come into consideration are especiallyhydroxyl-group-containing fibrous materials, including but not limitedto natural fibrous materials such as cotton, linen and hemp, andregenerated fibrous materials such as viscose and lyocell. Furtherfibrous materials include wool, silk, polyvinyl, polyacrylonitrile,polyamide, aramide, polypropylene and polyurethane. The said fibrousmaterials are preferably in the form of sheet-form textile wovenfabrics, knitted fabrics or webs.

Suitable commercially available inkjet printers designed for textileprinting include, for example, DuPont® Artistri® 2020 and 3210 TextilePrinters (E.I. du Pont de Nemours and Company, Wilmington, Del.),Textile Jet (Mimaki USA, Duluth, Ga.), DisplayMaker Fabrijet (MacDermidColor Span, Eden Prairie, Minn.), Amber, Zircon, and Amethyst (Stork®).

The printed textiles may optionally be post processed with heat and/orpressure, such as disclosed in US20030160851.

Upper temperature is dictated by the tolerance of the particular textilebeing printed. Lower temperature is determined by the amount of heatneeded to achieve the desired level of durability. Generally, fusiontemperatures will be at least about 80° C. and preferably at least about140° C., more preferably at least about 160° C. and most preferably atleast about 180° C.

Fusion pressures required to achieve improved durability can be verymodest. Thus, pressures can be about 3 psig, preferably at least about 5psig, more preferable at least about 8 psig and most preferably at leastabout 10 psig. Fusion pressures of about 30 psi and above seem toprovide no additional benefit to durability, but such pressures are notexcluded.

The duration of fusion (amount of time the printed textile is underpressure at the desired temperature) is not believed to be particularlycritical. Most of the time in the fusion operation generally involvesbringing the print up to the desired temperature. Once the print isfully up to temperature, the time under pressure can be brief (seconds).

This invention is further illustrated, but not limited, by the followingExamples.

EXAMPLES

Tests used to characterize the polyurethane dispersoids, the inks andthe printed textiles were those commonly used in the art. Some specificprocedures are listed

Printing and Testing Techniques

Inkjet printers used in the following examples were:

(1) a print system with a stationery print head mount with up to 8 printheads, and a media platen. The printheads were from Xaar (Cambridge,United Kingdom). The media platen held the applicable media and traveledunderneath the print heads. The sample size was 7.6 cm by 19 cm. Unlessotherwise noted this print system was used to print the test samples.

(2) Seiko IP-4010 printer configured to accept fabrics

(3) DuPont® Artistri® 2020 printer.

The fabrics used were obtained from Testfabrics, Inc, (Pittston Pa.)namely: (1) 100% cotton fabric style #419W, which is a bleached,mercerized combed broadcloth (133×72); (2) Polyester/cotton fabric style#7435M, which is a 65/35 poplin mercerized and bleached; and (3)Polyester fabric style 7436, which is a 65/35 poplin mercerized andbleached.

In some examples, the printed textile was fused at elevated temperatureand pressure. Two different fusing apparatus were employed:

(1) a Glenro (Paterson, N.J.) Bondtex™ Fabric and Apparel Fusing Presswhich moves the printed fabric between two heated belts equipped withadjustable pneumatic press and finally through a nip roller assembly;and

(2) a platen press, assembled for the purpose of precisely controllingtemperature and pressure. The platen press was comprised of two parallel6″ square platens with embedded resistive heating elements that could beset to maintain a desired platen temperature. The platens were fixed ina mutually parallel position to a pneumatic press that could press theplatens together at a desired pressure by means of adjustable airpressure. Care was taken to be sure the platens were aligned so as toapply equal pressure across the entire work piece being fused. Theeffective area of the platen could be reduced, as needed, by inserting aspacer (made, for example from silicone rubber) of appropriatedimensions to allow operation on smaller work pieces.

The standard temperature for the fusing step in the examples was 160° C.unless otherwise indicated.

The printed textiles were tested according to methods developed by theAmerican Association of Textile Chemists and Colorists, (AATCC),Research Triangle Park, N.C. The AATCC Test Method 61-1996,“Colorfastness to Laundering, Home and Commercial: Accelerated”, wasused. In that test, colorfastness is described as “the resistance of amaterial to change in any of its color characteristics, to transfer ofits colorant(s) to adjacent materials or both as a result of theexposure of the material to any environment that might be encounteredduring the processing, testing, storage or use of the material.” Test 3Awas done and the color washfastness was recorded. The ratings for thesetests are from 1-5 with 5 being the best result, that is, little or noloss of color.

Colorfastness to crocking was also determined by AATCC CrockmeterMethod, AATCC Test Method 8-1996. The ratings for these tests were from1-5 with 5 being the best result, that is, little or no loss of colorand little or no transfer of color to another material, respectively.The results are rounded to the nearest 0.5, which was judged to beaccuracy of the method.

The colorant dispersion, or other stable aqueous colorant, was preparedby techniques known in the inkjet art. A black pigment dispersion wasused for the ink examples except where noted. The following ingredientswere used as indicated to form the crosslinked polyurethanes used in theexamples.

Ingredients and Abbreviations

BZMA=benzyl methacrylate

DBTL=dibutyltindilaurate

DMEA=dimethylethanolamine

DMIPA=dimethylisopropylamine

DMPA=dimethylol propionic acid

EDA=ethylene diamine

ETEGMA=ethoxytriethylenglycolmethacrylate

HDI=1,6-hexamethylene diisocyanate

IPDA=isophoronediamine

IPDI=isophoronediisocyanate

MAA=methyl acrylic acid

POEA=2-phenoxyethyl acrylate ester

TEA=triethylamine

TETA=triethylenetetramine

THF=tetrahydrofuran

Unless otherwise noted, the above chemicals were obtained from Aldrich(Milwaukee, Wis.) or other similar suppliers of laboratory chemicals.

Desmophene C 200—a polyester carbonate diol from Bayer (Pittsburgh, Pa.)

Surfynol® 440—a nonionic surfactant from Air Products (Allentown, Pa.)

Terathane® 1400—a polytetramethylene oxide polyol from Invista(Wilmington, Del.)

Extent of Polyurethane Reaction

The extent of polyurethane reaction was determined by detecting NCO % bydibutylamine titration, a common method in urethane chemistry. In thismethod, a sample of the NCO containing prepolymer is reacted with aknown amount of dibutylamine solution and the residual amine is backtitrated with HCl.

Particle Size Measurements

The particle size for the polyurethane dispersions, pigments and theinks were determined by dynamic light scattering using a Microtrac® UPA150 analyzer from Honeywell/Microtrac (Montgomeryville Pa.).

This technique is based on the relationship between the velocitydistribution of the particles and the particle size. Laser generatedlight is scattered from each particle and is Doppler shifted by theparticle Brownian motion. The frequency difference between the shiftedlight and the unshifted light is amplified, digitalized and analyzed torecover the particle size distribution.

The reported numbers below are the volume average particle size.

Solid Content Measurement

Solid content for the solvent free or the aqueous crosslinkedpolyurethane dispersoids was measured with a moisture analyzer, modelMA50 from Sartorius. For polyurethane dispersoid containing high boilingsolvent, such as NMP, the solid content was then determined by theweight differences before and after baking in 150° C. oven for 180minutes. It should be noted that a polyurethane which is dried in thismanner to its solid cannot be easily redispersed and used.

THF Insolubles Measurement

THF insolubles content of the polyurethanes was measured by first mixing1 gram of the polyurethane dispersoid with 30 grams of THF in apre-weighed centrifuge tube. After the solution was centrifuged for 2hours at 17,000 rpm, the top liquid layer was poured out and thenon-dissolved gel in the bottom was left. The centrifuge tube with thenon-dissolved gel was re-weighed after the tube was put in the oven anddried for 2 hours at 110° C.

% Micro-gel of polyurethane=((weight of tube and non-dissolvedgel)−(weight of tube))/(sample weight*polyurethane solid %).

Test for Hydrolytic Stability of the Polyurethanes

A test for studying the hydrolytic stability of a polyurethane is tocast a film of the polyurethane from its dispersion, soak the film inwater and then measure the increase in weight. The test is done withfreshly prepared polyurethanes and polyurethanes that had been heat agedby putting the polyurethane dispersion in an oven at 70° C. for sevendays. The weight increase, the water uptake, is compared for the freshpolyurethane and the aged material. If the polyurethane degrades underthe aging conditions, that degradation can be attributed to thehydrolysis of some of the bonds in the polyurethane.

If the water uptake of film made from aged polyurethane is similar tothe film from fresh polyurethane, then this indicates a relatively goodhydrolytic stability; and, in turn, long term stability of thepolyurethane dispersion or an ink jet ink made from the dispersion.

PUD Film Preparation

10-20 g of PUD resin was poured into a Petri dish lined with Teflonfilm. The resin was allowed to air dry for 48 hours first. Then it wasbaked in vacuum oven at 100° C. for 4 hours. The thickness of the driedfilm ranged from about 1 mm to 3.5 mm.

Water Up-Take Test

0.5 to 1.0 g of resin film was place in a 1 oz glass jar. The glass jarwas filled with 30 g detergent water to cover the film. (1.5 g AATCC 3Awash detergent per liter water). The glass jar was then placed in ovenat 70 C for 24 hours. Immediately after the glass jar was removed fromthe oven, the film was taken out, dried with a golf towel and weighed.

Water up-take %=(weight after water immersion−original weight)/originalweight

Preparation of Inks

Inks used in the examples were made according to standard procedures inthe inkjet art. Ingredient amounts are in weight percent of the finalink. Polyurethane dispersoid binders and colorants are quoted on asolids basis.

As an example of ink preparation, the ink vehicle was prepared and addedwith stirring to the aqueous dispersion polyurethane dispersoid binders.After stirring until a good dispersion was obtained, the mixture wasthen added to the pigment dispersion and stirred for another 3 hours, oruntil a good ink dispersion was obtained.

Preparation of Black Pigment Dispersion

A black dispersion was prepared by first mixing well the followingingredients: (i) 210.4 parts by weight (pbw) deionized water, (ii) 80.3pbw of a 41.5 wt % (solids) anionic polymeric dispersant, and (iii) 9.24pbw of dimethylethanolamine. The anionic polymer dispersant was a graftco-polymer 66.3/-g-4.2/29.5 POEA/-g-ETEGMA/MAA prepared according to“Preparation of Dispersant 1” from US20030128246, with the ratios ofmonomers adjusted to obtain the 66.2/4.2/29.5 instead of the61.6/5.8/32.6 ratio indicated in the publication.

To this was gradually added 100 pbw black pigment (Nipex 180IQ,Degussa). After the pigment was incorporated, 100 pbw deionized waterwas mixed in to form the millbase, which was circulated through a mediamill for grinding. 55.4 pbw deionized water was then added for dilutionto final strength.

The resulting 15 wt % dispersion had the following properties: aviscosity of 8.60 cP (Brookfield viscometer, 20° C.), a pH of about 7.5and a median particle size of 92 nm.

Crosslinked Polyurethane Dispersion Comparative Example 1

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 699.2 gDesmophene C 1200, a polyester carbonate diol (Bayer), 280.0 g acetoneand 0.06 g DBTL. The contents were heated to 40° C. and mixed well.189.14 g IPDI was then added to the flask via the addition funnel at 40°C. over 60 min, with any residual IPDI being rinsed from the additionfunnel into the flask with 15.5 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 44.57 g DMPA, then followed by 25.2 g TEA, was added to theflask via the addition funnel, which was then rinsed with 15.5 gacetone. The flask temperature was then raised again to 50° C. and heldat 50° C. until NCO % was 1.23% or less.

With the temperature at 50° C., 1498.0 g deionized (DI) water was addedover 10 minutes, followed by mixture of 97.5 g EDA (as a 6.25% solutionin water) and 29.7 g TETA (as a 6.25% solution in water) over 5 minutes,via the addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−310.0 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion Comparative Example 2

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 349 gFormrez66-56, a 2000 MW poly(hexaneadipate) diol (Crompton), 140 gacetone and 0.06 g DBTL. The contents were heated to 40° C. and mixedwell. Mixture of 87 g IPDI and 16 g Desmodur N3400 was then added to theflask via the addition funnel at 40° C. over 60 min, with any residualIPDI being rinsed from the addition funnel into the flask with 10 gacetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 22.3 g DMPA, then followed by 12.8 g TEA, was added to theflask via the addition funnel, which was then rinsed with 6.7 g acetone.The flask temperature was then raised again to 50° C. and held at 50° C.until NCO % was 1.22% or less.

With the temperature at 50° C., 750 g deionized (DI) water was addedover 10 minutes, followed by 90 g EDA (as a 6.25% solution in water)over 5 minutes, via the addition funnel, which was then rinsed with 40.0g water. The mixture was held at 50° C. for 1 hr, then cooled to roomtemperature.

Acetone (−160 g) was removed under vacuum, leaving a final dispersion ofpolyurethane with about 35.0% solids by weight

Crosslinked Polyurethane Dispersion Comparative Example 3

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 663.6 g Terathane1400, a polyether diol (Invista), 280.0 g acetone and 0.06 g DBTL. Thecontents were heated to 40° C. and mixed well. 223.5 g IPDI was thenadded to the flask via the addition funnel at 40° C. over 60 min, withany residual IPDI being rinsed from the addition funnel into the flaskwith 15.5 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 44.5 g DMPA, then followed by 25.2 g TEA, was added to theflask via the addition funnel, which was then rinsed with 15.5 gacetone. The flask temperature was then raised again to 50° C. and heldat 50° C. until NCO % was 1.23% or less.

With the temperature at 50° C., 1415 g deionized (DI) water was addedover 10 minutes, followed by mixture of 26.2 g EDA (as a 6.25% solutionin water) and 212.4 g TETA (as a 6.25% solution in water) over 5minutes, via the addition funnel, which was then rinsed with 80.0 gwater. The mixture was held at 50° C. for 1 hr, then cooled to roomtemperature.

Acetone (−310.0 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion Comparative Example 4

To a dry alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line, was added 349.6 g of PCDLL6002, a polycarbonate diol, (Asahi Kasei), 140 g acetone and 0.04 gDBTL. The contents were heated to 40° C. and mixed well. 87 g IPDI, 16 gDesmodur N3400, a HDI 40 wt % dimer and 60 wt % trimer blend, (Bayer)were then charged to the flask via the addition funnel over 60 min, withany residual isocyanate being rinsed from the addition funnel into theflask with 10 g acetone.

The flask temperature was raised to 50° C. and held for 30 minutes. 22.3g DMPA followed by 12.8 g TEA was then added to the flask via theaddition funnel, which was then rinsed with 10 g of acetone. The flasktemperature was held at 50° C. until NCO % was 1.25% or less.

With temperature at 50° C., 750.0 g DI water was added over 10 minutes,followed by 90 g EDA (as a 6.25% solution in water) over 5 minutes, viathe addition funnel, which was then rinsed with 40.0 g of water. Themixture was then held at 50° C. for 1 hr, then cooled to roomtemperature.

Acetone (−160 g) was removed under vacuum, leaving a final dispersion ofpolyurethane with about 35% solids by weight.

Crosslinked Polyurethane Dispersion 1

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 655.3 g PCDLT6002, a polycarbonate diol (Asahi Kasei), 152.7 g Terathane 1400, apolyether diol (Invista), 326.6 g acetone and 0.08 g DBTL. The contentswere heated to 40° C. and mixed well. 228.7 g IPDI was then added to theflask via the addition funnel at 40° C. over 60 min, with any residualIPDI being rinsed from the addition funnel into the flask with 18 gacetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 52 g DMPA, then followed by 32 g DMIPA (dimethyl isopropylamine), was added to the flask via the addition funnel, which was thenrinsed with 18 g acetone. The flask temperature was then raised again to50° C. and held at 50° C. until NCO % was 1.17% or less.

With the temperature at 50° C., 1750.5 g deionized (DI) water was addedover 10 minutes, followed by mixture of 29 g EDA (as a 6.25% solution inwater) and 139 g DETA (as a 6.25% solution in water) over 5 minutes, viathe addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−362.6 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 2

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 718.9 g PCDLT6002, a polycarbonate diol (Asahi Kasei), 90.4 g Terathane 1400, apolyether diol (Invista), 326.6 g acetone and 0.08 g DBTL. The contentswere heated to 40° C. and mixed well. 226.9 g IPDI was then added to theflask via the addition funnel at 40° C. over 60 min, with any residualIPDI being rinsed from the addition funnel into the flask with 18 gacetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 52 g DMPA, then followed by 27 g DMIPA (dimethyl isopropylamine), was added to the flask via the addition funnel, which was thenrinsed with 18 g acetone. The flask temperature was then raised again to50° C. and held at 50° C. until NCO % was 1.17% or less.

With the temperature at 50° C., 1719.4 g deionized (DI) water was addedover 10 minutes, followed by mixture of 29 g EDA (as a 6.25% solution inwater) and 141 g TETA (as a 10.4% solution in water) over 5 minutes, viathe addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−362.6 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 3

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 715 g PCDL T6002,a polycarbonate diol (Asahi Kasei), 78.8 g Terathane 650, a polyetherdiol (Invista), 326.3 g acetone and 0.08 g DBTL. The contents wereheated to 40° C. and mixed well. 241.9 g IPDI was then added to theflask via the addition funnel at 40° C. over 60 min, with any residualIPDI being rinsed from the addition funnel into the flask with 18 gacetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 52 g DMPA, then followed by 27 g DMIPA (dimethyl isopropylamine), was added to the flask via the addition funnel, which was thenrinsed with 18 g acetone. The flask temperature was then raised again to50° C. and held at 50° C. until NCO % was 1.24% or less.

With the temperature at 50° C., 1719.4 g deionized (DI) water was addedover 10 minutes, followed by mixture of 30.8 g EDA (as a 6.25% solutionin water) and 150 g TETA (as a 10.4% solution in water) over 5 minutes,via the addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−362.3 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 4

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 301.7 g Sovermol920, a polyether carbonate diol, (Cognis), 121.3 g acetone and 0.06 gDBTL. The contents were heated to 40° C. and mixed well. 83.7 g IPDI wasthen added to the flask via the addition funnel at 40° C. over 60 min,with any residual IPDI being rinsed from the addition funnel into theflask with 6.7 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 19.3 g DMPA, then followed by 10.9 g TEA, was added to theflask via the addition funnel, which was then rinsed with 6.7 g acetone.The flask temperature was then raised again to 50° C. and held at 50° C.until NCO % was 1.05% or less.

With the temperature at 50° C., 652 g deionized (DI) water was addedover 10 minutes, followed by mixture of 10.8 g EDA (as a 6.25% solutionin water) and 52.5 g TETA (as a 6.25% solution in water) over 5 minutes,via the addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−134.7 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 5a (Z₂ and Z₃ Diols Only)

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 815.8 g PCDLT6002, a polycarbonate diol (Asahi Kasei), 326.5 g acetone and 0.08 gDBTL. The contents were heated to 40° C. and mixed well. 220.67 g IPDIwas then added to the flask via the addition funnel at 40° C. over 60min, with any residual IPDI being rinsed from the addition funnel intothe flask with 18 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 52 g DMPA, then followed by 31.3 g TEA was added to theflask via the addition funnel, which was then rinsed with 18 g acetone.The flask temperature was then raised again to 50° C. and held at 50° C.until NCO % was 1.13% or less.

With the temperature at 50° C., 1754 g deionized (DI) water was addedover 10 minutes, followed by mixture of 29.2 g EDA (as a 6.25% solutionin water) and 120.7 g DETA (as a 6.25% solution in water) over 5minutes, via the addition funnel, which was then rinsed with 80.0 gwater. The mixture was held at 50° C. for 1 hr, then cooled to roomtemperature.

Acetone (−362.5 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 5b (Z₁ and Z₂ Diols Only)

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 774.2 g Terathane1400, a polyether diol (Invista), 326.1 g acetone and 0.08 g DBTL. Thecontents were heated to 40° C. and mixed well. 260.7 g IPDI was thenadded to the flask via the addition funnel at 40° C. over 60 min, withany residual IPDI being rinsed from the addition funnel into the flaskwith 18 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 52 g DMPA, then followed by 31.3 g TEA was added to theflask via the addition funnel, which was then rinsed with 18 g acetone.The flask temperature was then raised again to 50° C. and held at 50° C.until NCO % was 1.33% or less.

With the temperature at 50° C., 1717.8 g deionized (DI) water was addedover 10 minutes, followed by mixture of 36 g EDA (as a 6.25% solution inwater) and 148.9 g DETA (as a 6.25% solution in water) over 5 minutes,via the addition funnel, which was then rinsed with 80.0 g water. Themixture was held at 50° C. for 1 hr, then cooled to room temperature.

Acetone (−362.1 g) was removed under vacuum, leaving a final dispersionof polyurethane with about 35.0% solids by weight.

Crosslinked Polyurethane Dispersion 6b (Z₂ and Z₃ Diols Only)

To a dry, alkali- and acid-free flask, equipped with an addition funnel,a condenser, stirrer and a nitrogen gas line was added 220.0 g TegoBD1000, a 1000 MW butylmethacrylate diol, (Degussa), 108 g acetone and0.06 g DBTL. The contents were heated to 40° C. and mixed well. Mixture87 g IPDI and 16 g Desmodur N3400 was then added to the flask via theaddition funnel at 40° C. over 60 min, with any residual being rinsedfrom the addition funnel into the flask with 10 g acetone.

The flask temperature was raised to 50° C., held for 30 minutes thenfollowed by 18 g DMPA, then followed by 10 g TEA, was added to the flaskvia the addition funnel, which was then rinsed with 10 g acetone. Theflask temperature was then raised again to 50° C. and held at 50° C.until NCO % was 1.35% or less.

With the temperature at 50° C., 588 g deionized (DI) water was addedover 10 minutes, followed by 74.9 g EDA (as a 6.25% solution in water)over 5 minutes, via the addition funnel, which was then rinsed with 80.0g water. The mixture was held at 50° C. for 1 hr, then cooled to roomtemperature.

Acetone (−128 g) was removed under vacuum, leaving a final dispersion ofpolyurethane with about 35.0% solids by weight.

Water Up-Take Testing of Polyurethanes

Films of freshly made polyurethanes and heat aged were made and testedin the water up-take test. The test results are reported in Table 1below.

TABLE 1 Water Up-take Test Water up-take % Water-up-take % for for filmprepared Film prepared after from fresh made dispersion aged atdispersions 70 C. for 7 days % change Comparative 70% 150%  114%  Ex 1Comparative 70% Film dissolved NA Ex 2 Comparative 110%  200%  82% Ex 3Comparative 45% 65% 45% Ex 4 PUD EX6b 42% 65% 54% (Comp EX 5)(1) PUD EX156% 86% 53% PUD EX2 50% 75% 50% PUD EX3 112%  116%  3.6%  PUD EX4 82%92% 12% (1)When PUD example 6b is used alone it is a comparative examplesince it has a PUD with only Z₂ and Z₃.

The Comparative Example 1 showed dramatic water uptake increase betweenthe film cast from the fresh polyurethane and the aged polyurethane.Comparative Example 2 showed an high water uptake and after thecorresponding polyurethane dispersion was heat aged and cast as a filmthe film was soluble in the water. Comparative Example 3 showed highwater uptake and poor wash fastness (Table 3). Comparative Example 4 and5 while showing adequate water uptake for both the freshly made and theaged material displayed other poorer printing attributes, including apoor crock, poor hand of the printed textile when compared to theinventive examples, This inventive inks took up less water suggestingthat there stability to water is better.

Black inks were made with the comparative and the inventive crosslinkedpolyurethane dispersoids. The black dispersion was previously describedand has 4.25% black dispersion in each ink. These inks were printed onto419 Cotton and tested for washfastness and Crock by the AATC method.

TABLE 2 Black ink Formulations Comp Comp Comp ink A ink B ink C A B C DE F Comp  9% PUD 1 Comp  8% PUD 3 Comp 13% PUD 4 PUD EX1  9% PUD EX2  9%PUD EX3  9% PUD EX4 13% PUD 7.20% 8.10% EX5A PUD 1.80% 0.90% EX5BGlycerol 18% 18%  8% 18% 18% 18%  8%   18%   18% Ethylene 12% 12% 12%12% 12% 12% 12%   12%   12% Glycol Surfynol 1.00%   1.00%   1.00%  1.00%   1.00%   1.00% 1.00% 440 Surfynol 0.15%   0.15%   104E Silwet0.15%   0.15%   L77 Water (to Bal Bal Bal Bal Bal Bal Bal Bal Bal 100%)Viscosity 7.4 7.73 7.95 8.68 10 8.2 7.55 8 7.8 (cps)

TABLE 3 Crock and wash fastness results for black ink examples Inkexample Comp Comp Comp Ink 1 Ink 2 Ink 3 A B C D E F Dry crock 4.5 4 3.54.5 4.5 4.5 4.5 4.5 4.5 Wet crock 2.5 2.5 2 2.5 3 3 2.5 3 2.5 3A 4.5 2.54.5 4.5 5 4.5 4 4.5 4 washfastness

In initial tests the comparative ink and the inventive examples havecomparable washfastness and crock.

The Comparative Ink 1 and Inventive Examples A, B and C were stored in aheated oven at 50° C. for 12 weeks or 40° C. for 16 weeks and thenprinted on cotton and tested for crock and wash fastness.

TABLE 4 Washfastness results for oven aged black ink Ink example CompInk 1 A B C Initial 3A washfasness 4.0 4.5 5.0 4.5 3A washfasness afterink 1.0 3.5 4.5 4.5 stored at 50° C. 12 weeks 3A washfasness after ink2.5 4.5 4.5 4.0 stored at 40° C. 16 weeks 40° C.

The inventive inks are superior to the Comparable Ink. Even under thesemodest storage conditions that inks might experience commercially, theinventive inks did not exhibit any degradation based on these tests.While not being bound by theory, the inventive inks appear to be stableto hydrolysis conditions that would exist in an aqueous ink jet ink.

A further confirmation of the degradation of the crosslinkedpolyurethane dispersoids is the measure of the loss of the microgelscontent as measured by the THF solubles test.

TABLE 5 Micro-gel content results for oven aged binder Comparative PUDPUD PUD PUD Ex 1 Ex 1 Ex 2 Ex 3C Initial Microgel % 4.3% 3.1% 6.5% 10.1%Microgel % after binder 1.3% 2.3% 4.1% 8.1% stored at 50° C. 6 weeks %drop  70%  26%  36% 19.8%

The comparative crosslinked polyurethane dispersoid loses asubstantially amount of the microgels after heat aging. While not beingbound by theory, the inventive inks appear to be more stable in thetest.

Colored inks were prepared using the following formulation with PUD EX 1These were printed Ink was printed with a Artistri® 2020 printer on 419100% cotton.

TABLE 6 Colored Ink Formulation Ink Color Cyan Magenta Yellow Blue Cyandispersion 3.0% (% pigment) Magenta dispersion 4.25%  (% pigment) Yellowdispersion 4.25%  (% pigment) Blue dispersion 3.0% (% pigment) Orangedispersion (% pigment) PUD EX 1 7.0% 7.5% 7.5% 7.5% Dipropylene Glycol  5%   2%   3%   3% Methyl Ether Glycerol  27%  18%  22%  18% EthyleneGlycol   8%   8%   8%   8% Surfynol 440 1.0% 1.0% 1.0% 1.0% Water (to100%) Balance Balance Balance Balance

TABLE 7 Crock and washfastness results of colored inks Dry Wet 3A InkExample Binder crock crock washfastness Cyan Ink I Comp 4.0 3.0 3.5 CyanInk J PUD EX1 4.5 3.5 4.0 Magenta Ink K Comp 4.0 3.0 3.0 Magenta Ink LPUD EX1 4.5 3.0 3.0 Yellow Ink M Comp 3.5 3.0 4.5 Yellow Ink N PUD EX14.0 3.5 4.0 Blue Ink O Comp 4.5 3.0 2.5 Blue Ink P PUD EX1 4.5 3.5 2.5

The inventive inks produced at least comparable print test results.These were tested as prepared and were not aged.

Samples of inventive black Ink were printed with an EPSON3000 printer onHammermill Copy Plus (HCP) paper and Xerox 4024 paper. To determinewaterfastness, a pattern consisting of five 4 mm-wide parallel stripesspaced 7 mm apart is printed at 720 dpi. Holding the paper at an inclineof about 45 degrees, two drops of water—one on top of the other—areallowed to drip across the five printed stripes. This process is carriedout on different parts of the test pattern at 30 sec, 1 minute and 5minutes after printing. The stripes are rated OK if no indication of inkrunning.

TABLE 8 Ink composition Ink Q R Black SDP 6.0% 6.0% (% pigment) Compbinder 1.0% Crosslinked Polyurethane 1.0% Dispersoid EX1 Glycerol  18% 18% Ethylene Glycol   8%   8% Surfynol 440 1.0% 1.0% Water (to 100%)Balance Balance

TABLE 9 Waterfastness results HCP HCP HCP Xerox 4024 Xerox 4024 Xerox4024 Ink 30 sec 1 min 5 min 30 sec 1 min 5 min Ink Q OK OK OK OK OK OKInk R OK OK OK OK OK OK

The inventive inks passed this water fastness test for paper.

1. An inkjet ink composition comprising an aqueous vehicle having acolorant and a first crosslinked polyurethane dispersoid, wherein theink comprises the crosslinked polyurethane dispersoid in an amount ofmore than about 0.5% to about 30% by weight, based on the total weightof the ink, and wherein the amount of crosslinking in the crosslinkedpolyurethane is greater than about 1% and less than about 50 wt % asmeasured by the THF insolubles test and where the crosslinkedpolyurethane is formed from at least a first diol, Z₁ a second diol, Z₂and a third diol Z₃ and where

p greater than or equal to 2, and m greater than or equal to 3 to about36; R₅, R₆=hydrogen, alkyl, substituted alkyl, aryl; where the R₅ or R₆are the same or different for each substituted methylene group and whereR₅ and R₅ or R₆ can be joined to form a cyclic structure; Z₂ is a diolsubstituted with an ionic group; Z₃ is selected from the groupconsisting of polycarbonate diols, polyamide diols andpoly(meth)acrylate diols; and where the colorant is selected frompigments and dyes or combinations of pigments and dyes.
 2. An inkjet inkcomposition comprising an aqueous vehicle having a colorant and a secondcrosslinked polyurethane dispersoid and a third crosslinked polyurethanedispersoid, wherein the ink comprises the second crosslinkedpolyurethane dispersoid in an amount of more than about 0.25% to about30% by weight based on the total weight of the ink, and the thirdcrosslinked polyurethane dispersoid in an amount of more than about 0.5%to about 30% by weight based on the total weight of the ink wherein theamount of crosslinking in the second crosslinked polyurethane is greaterthan about 1% and less than about 50 wt % as measured by the THFinsolubles test and the amount of crosslinking in the third crosslinkedpolyurethane is greater than about 1% and less than about 50 wt % asmeasured by the THF insolubles test where the second crosslinkedpolyurethane is formed from at least a first diol, Z₁ and a second diol,Z₂ and the third crosslinked polyurethane is formed from at least asecond diol, Z₂ and a third diol, Z₃ and where

p greater than or equal to 2, and m greater than or equal to 3 to about36; R₅, R₆=hydrogen, alkyl, substituted alkyl, aryl; where the R₅ or R₆are the same or different for each substituted methylene group and whereR₅ and R₅ or R₆ can be joined to form a cyclic structure; Z₂ is a diolsubstituted with an ionic group; Z₃ is selected from the groupconsisting of polycarbonate diols, polyamide diols andpoly(meth)acrylate diols; and where the colorant is selected frompigments or dyes or combinations of pigments and dyes.
 3. The inkjet inkcomposition of claim 1, having a surface tension in the range of about20 dyne/cm to about 70 dyne/cm, and a viscosity in the range of about 1cP to about 30 cP at 25° C.
 4. The inkjet ink composition of claim 1,wherein the colorant comprises a pigment.
 5. The inkjet ink compositionof claim 1, wherein the first crosslinked polyurethane comprises diolsZ₁ Z₂ and Z₃ and Z₃ is a polycarbonate diol.
 6. The inkjet compositionof claim 1, wherein the first crosslinked polyurethane is formed fromdiols Z₁, Z₂ and Z₃ and the mole ratio of diols Z₁, and Z₃ is about 1:1to about 1:10.
 7. The inkjet composition of claim 1, wherein the firstcrosslinked polyurethane is formed from diols Z₁, Z₂ and Z₃ and the moleratio of diols Z₁, and Z₃ is about 1:1.5 to about 1:7.
 8. A method forinkjet printing onto a substrate, comprising the steps of: (a) providingan inkjet printer that is responsive to digital data signals; (b)loading the printer with a substrate to be printed; (c) loading theprinter with an ink as set forth in any one of claims 1 and 2; and (d)printing onto the substrate using the ink or inkjet ink set in responseto the digital data signals.
 9. The method of claim 8, wherein thesubstrate is a textile.
 10. The method of claim 9, wherein the printedsubstrate is post treated with a combination of heat and pressure. 11.The inkjet ink composition of claim 2, having a surface tension in therange of about 20 dyne/cm to about 70 dyne/cm, and a viscosity is in therange of about 1 cP to about 30 cP at 25° C.
 12. The inkjet inkcomposition of claim 2, wherein the colorant comprises a pigment. 13.The inkjet ink composition of claim 2, wherein the third crosslinkedpolyurethane is formed from diols Z₂ and Z₃ and Z₃ is a polycarbonatediol.
 14. The inkjet composition of claim 2, wherein the second andthird crosslinked polyurethanes are formed from diols Z₁ and, Z₂ and Z₂and Z₃ respectively and the mole ratio of diols Z₁, and Z₃ is about 1:1to about 1:10.
 15. The inkjet composition of claim 2, wherein the secondand third crosslinked polyurethanes are formed from diols Z₁ and Z₂ andZ₂ and Z₃ respectively and the mole ratio of diols Z₁, and Z₃ is about1:1.5 to about 1:7.